US4826910A - Oil resistant thermoplastic elastomer - Google Patents
Oil resistant thermoplastic elastomer Download PDFInfo
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- US4826910A US4826910A US07/119,099 US11909987A US4826910A US 4826910 A US4826910 A US 4826910A US 11909987 A US11909987 A US 11909987A US 4826910 A US4826910 A US 4826910A
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L13/00—Compositions of rubbers containing carboxyl groups
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/09—Carboxylic acids; Metal salts thereof; Anhydrides thereof
- C08K5/098—Metal salts of carboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/14—Peroxides
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L27/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
- C08L27/02—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L27/04—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
- C08L27/06—Homopolymers or copolymers of vinyl chloride
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
- C08L67/04—Polyesters derived from hydroxycarboxylic acids, e.g. lactones
Definitions
- This invention relates to an oil resistant thermoplastic elastomer composition which contains carboxylated nitrile rubber, polyvinyl chloride and polycaprolactone.
- Thermoplastic elastomer compositions are well known. Such compositions have a high melt flow property that allows them to be processed as thermoplastic materials, yet they also demonstrate certain rubbery characteristics.
- U.S. Pat. No. 3,037,954 teaches a process to prepare a thermoplastic elastomer in which polypropylene and a rubber are subjected to "dynamic curing conditions".
- the examples of the patent illustrate that the products produced according to the patent demonstrate the properties of thermoplastic elastomers.
- the present invention provides a process for preparing an oil resistant thermoplastic elastomer composition comprising admixing
- the admixing being at a temperature above the activation temperature of the peroxy curing agent, for a sufficient length of time to cause admixing and vulcanization but not to cause significant thermal degradation of components (i), (ii) or (iii).
- thermoplastic elastomer compositions produced according to the process of the present invention exhibit good oil resistance and a good balance between compression set and melt flow index properties.
- the polyvinyl chloride used in the present invention may be any polyvinyl chloride resin known in the art. However, it is preferred to use a low molecular weight polyvinyl chloride which provides easy processing. Polyvinyl chloride sold under the trade name Esso PVC 360 by Esso Chemical Canada has been found to provide satisfactory results when used in the present invention.
- the carboxylated nitrile rubber used in the present invention may be any of those known in the art. These are copolymers of butadiene, acrylonitrile and one or more ⁇ , ⁇ unsaturated carboxylic acids.
- the carboxylic acids may contain one or more carboxylic groups. Because of cost and availability, it is preferred that the carboxylic acids be selected from acrylic, methacrylic, fumaric, maleic and itaconic acids.
- the copolymers may be prepared by the well known emulsion free radical process.
- the acrylonitrile content of the copolymer may be from about 20 to about 40 percent by weight.
- the total content of the carboxylic acid in the copolymer may be from about 0.5 to about 10 percent by weight. Butadiene forms the balance to 100 weight percent of the copolymer.
- the viscosity of the carboxylated nitrile rubber is generally within the Mooney range (M L 1+4 at 100° C.) of from about 40 to about 80.
- the polycaprolactone is a linear polyester which is formed by a ring opening polymerization of epsilon-caprolactone monomer.
- the polymer contains repeat units of the structure: ##STR1## where p is at least 100 but not more than 3000.
- the process of the present invention relates to a polymer composition which contains 20 to 50 weight percent carboxylated nitrile rubber polymer, 20 to 50 weight percent polyvinyl chloride polymer and 5 to 30 weight percent polycaprolactone polymer, with the term "weight percent” meaning exclusive of the weight of the other additives.
- Compositions which comprise 35 to 45 weight percent carboxylated nitrile rubber, 35 to 45 weight percent polyvinyl chloride and 10 to 20 weight percent polycaprolactone are preferred.
- peroxy curing agent as used herein is meant to refer to the well known peroxide and hydroperoxide curing agents.
- any of the conventional peroxy curing agents may be employed, including dicumyl peroxide, tertiary butyl peroxy benzoate, cumene hydroperoxide, 2,5 dimethyl-2,5 di(benzoyl peroxy) hexane, and benzoyl peroxide.
- the amount of peroxy curing agent should be from about 0.2 to 10 "parts by weight", wherein the term parts by weight refers to its conventional meaning, namely parts by weight per 100 parts by weight of total polymer. The preferred amount will depend upon the specific type of peroxy curing agent chosen. Skilled persons will be able to readily optimize curatives, using small scale experiments with less than 100 grams of polymer.
- the process of the present invention also requires the use of a crosslinking coagents.
- a crosslinking coagents Any of the coagents which may be employed in peroxy curing reactions are suitable for use in the present invention. Examples of such coagents include triethylene glycol dimethacrylate, trialkyl cyanurate, trialkyl phosphate, ethylene dimethacrylate, 1.2 polybutadiene, zinc acrylate and tetrahydrofurfuryl methacrylate.
- the amount of the coagent is from 3 to 20 parts by weight, preferably 5 to 10 parts by weight. Mixtures of more than one coagent may also be employed.
- the stabilizers used in the present invention may be one or more of the commercially available metal salts, organo metallic salts or soaps or organometallic compounds which are well known in the art. These stabilizers are frequently sold on a propietary basis, with their exact chemical composition not being disclosed. A description of available stabilizers which are used with PVC is given in Chapter 9 of "Encyclopedia of PVC", edited by L. I. Nass and published by Marcel Dekker Inc. Using the classification scheme described therein, suitable stabilizers for use in the present invention include lead salts, mixed metal salts, organotin stabilizers and organonickel stabilizers.
- Preferred stabilizers include the mixed metal salts of barium/cadmium, barium/cadmium/zinc, and barium/zinc and the organotin stabilizers.
- the total amount of stabilizers in a polymer blend for use in the process of the present invention is from about 1.0 to 4 parts by weight, preferably from about 1.5 to 3 parts by weight.
- the antioxidants for use in the present invention may be one or more of any of the antioxidants which are used in the art of compounding heat resistant, carboxylated nitrile rubber.
- Suitable antioxidants include p-cumyldiphenylamide, octylated diphenylamine, polymerized 1,2 dihydro-2,2,4-trimethylquinoline, nickel salts of dibutyl- and dimethyl-dithiocarbamate, mercaptobenzimidazole and its zinc salts 2-mercaptobenzimidazole and its zinc salts, tris(nonylated phenyl)phosphite, p-phenylenediamine derivatives, and hindered phenolic antioxidants such as thiodiethylene bis(3,5-di-t-butyl-4-hydroxy)hydro cinnamate.
- the total amount of antioxidats used in compositions of the present invention is from about 0.2 to 4 parts by weight. A mixture of more than one antioxidant may be used
- compositions prepared according to the present invention may optionally include further additives such as, for example, pigments, fillers, extender oils such as dioctyl phthalate and processing aids.
- further additives such as, for example, pigments, fillers, extender oils such as dioctyl phthalate and processing aids.
- the process of the invention is carried out by mixing the components in ordinary mixing equipment, such as mill roll mixers, banbury mixers, and screw mixers. The mixture is heated and kneaded at a temperature above the activation temperature of the peroxide. The temperature must be above the activation temperature of the peroxide in order for the dynamic curing reaction to proceed.
- the mixing process should not exceed about 210° C.
- the polymer composition is preferably mixed at a temperature of from about 145° to about 180° C., especially from about 160° to about 170° C.
- Preferred mixing times are from about 2 to about 30 minutes, especially from about 3 to about 10 minutes.
- Dynamically vulcanized compositions were prepared using the following procedure. Mixing was carried out in a labaoratory scale banbury mixer at 77 rpm. The ingredients shown in Table 2 were loaded at zero minutes with the banbury at a temperature of 82° C. and the heating steam on. Mixing was initiated and continued for a total time of 5-6 minutes. At a time when the mixing chamber temperature reached about 149° C., the ram was lifted and the banbury was brushed down. The dynamically cured compositions were dumped and sheeted using a laboratory mill mixer at a roll temperature of 120° C. The stock was then removed from the mill and allowed to cool.
- Cooled stock was then comminuted in a dicing machine and fed to an injection molding machine. Injection molding was completed in a 50 ton press machine, using the following conditions:
- Front zone temperature 300° F.
- Feed zone temperature 270° F.
- Dumbbell shaped samples were molded. Physical testing was carried out on the molded samples, according to ASTM D2240-81 (hardness); ASTM D412-80 (modulus, tensile strength and elongation); ASTM D395-78, at 70° C. (compression set), ASTM D1238 at 190° C. and 298.2 kPa (melt flow index) and ASTM D471-79 (fuel resistance).
- Comparative experiment 1 illustrates a dynamically vulcanized blend containing PVC and carboxylated nitrile rubber.
- the compression set of the composition is good.
- the melt flow index is fairly low. Accordingly, the vulcanized composition of comparative experiment 1 may be characterized as being elastomeric, but it should not be regarded as a thermoplastic elastomer.
- Inventive experiment 2 illustrates a dynamically vulcanized composition which displays a good balance between melt flow index and compression set.
- the physical properties of the composition of experiment 2 especially compression set, suggest a rubbery composition.
- the melt flow index shows that the composition may be readily molded or extruded.
- compositions which contain polyvinyl chloride, carboxylated nitrile rubber and a third resin.
- compositions of Table 3 were prepared according to the mixing procedures of example 1.
- composition of comparative experiment 10 contains SB copolymer and exhibits a relatively low melt flow index.
- compositions of comparative experiments 11 and 13 utilize 20 weight percent polypropylene and ethylene-vinyl acetate, respectively. Both compositions have an excellent melt flow index. However, the compression set of both compositions is higher than the compression set of the composition of inventive experiment 12.
- composition of inventive experiment 12 demonstrates a good balance between melt flow index and compression set.
- This example illustrates the effect of using different amounts of peroxy curing agent.
- Comparative experiment 20 was performed without any peroxide. Although the melt flow index of the resulting composition is excellent, the compression set is quite poor.
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Abstract
The present invention provides a process to prepare an oil resistant thermoplastic elastomer composition which contains carboxylated nitrile rubber, polyvinyl chloride and polycaprolactone.
Description
This invention relates to an oil resistant thermoplastic elastomer composition which contains carboxylated nitrile rubber, polyvinyl chloride and polycaprolactone.
Thermoplastic elastomer compositions are well known. Such compositions have a high melt flow property that allows them to be processed as thermoplastic materials, yet they also demonstrate certain rubbery characteristics.
U.S. Pat. No. 3,037,954 teaches a process to prepare a thermoplastic elastomer in which polypropylene and a rubber are subjected to "dynamic curing conditions". The examples of the patent illustrate that the products produced according to the patent demonstrate the properties of thermoplastic elastomers.
Simple blends of carboxylated nitrile rubber and polyvinyl chloride are also known. The blends are somewhat thermoplastic and are used in many molding applications. However, these blends do not typically exhibit the balance between rubbery properties and thermoplastic properties which is characteristic of thermoplastic elastomers.
More recently, flux blends of carboxylated nitrile rubber, polyvinyl chloride and nylon have been developed, as disclosed in U.S. Pat. No. 4,438,230. Vulcanizates of these blends are especially useful in applications where high tensile strength and retention of properties after ageing are required. The vulcanizates are somewhat rubbery, as illustrated by their relatively low compression set, but they do not exhibit the high melt flow of a thermoplastic.
It is an object of the present invention to provide a process to prepare an oil resistant, thermoplastic elastomer composition having a good balance between compression set and melt flow index properties.
The present invention provides a process for preparing an oil resistant thermoplastic elastomer composition comprising admixing
(i) from 20 to 50 weight percent carboxylated nitrile rubber
(ii) from 20 to 50 weight percent polyvinyl chloride
(iii) from 5 to 30 weight percent polycaprolactone, such that the total of (i), (ii) and (iii) is 100 weight percent
(iv) from 0.2 to 10 parts by weight peroxy curing agent
(v) from 3 to 10 parts by weight coagent for the peroxy curing agent
(vi) from 1 to 4 parts by weight stabilizer
(vii) from 0.2 to 4 parts by weight antioxidant,
the admixing being at a temperature above the activation temperature of the peroxy curing agent, for a sufficient length of time to cause admixing and vulcanization but not to cause significant thermal degradation of components (i), (ii) or (iii).
The thermoplastic elastomer compositions produced according to the process of the present invention exhibit good oil resistance and a good balance between compression set and melt flow index properties. The polyvinyl chloride used in the present invention may be any polyvinyl chloride resin known in the art. However, it is preferred to use a low molecular weight polyvinyl chloride which provides easy processing. Polyvinyl chloride sold under the trade name Esso PVC 360 by Esso Chemical Canada has been found to provide satisfactory results when used in the present invention.
The carboxylated nitrile rubber used in the present invention may be any of those known in the art. These are copolymers of butadiene, acrylonitrile and one or more α,β unsaturated carboxylic acids. The carboxylic acids may contain one or more carboxylic groups. Because of cost and availability, it is preferred that the carboxylic acids be selected from acrylic, methacrylic, fumaric, maleic and itaconic acids. The copolymers may be prepared by the well known emulsion free radical process. The acrylonitrile content of the copolymer may be from about 20 to about 40 percent by weight. The total content of the carboxylic acid in the copolymer may be from about 0.5 to about 10 percent by weight. Butadiene forms the balance to 100 weight percent of the copolymer.
The viscosity of the carboxylated nitrile rubber is generally within the Mooney range (ML 1+4 at 100° C.) of from about 40 to about 80. The polycaprolactone is a linear polyester which is formed by a ring opening polymerization of epsilon-caprolactone monomer. The polymer contains repeat units of the structure: ##STR1## where p is at least 100 but not more than 3000. Such polymers, and methods of their production, are well known to persons skilled in the relevant art.
It is a conventional practice to quantitatively define polymer blends on the basis of the weight percent of the polymer components, excluding other additives. Accordingly, the process of the present invention relates to a polymer composition which contains 20 to 50 weight percent carboxylated nitrile rubber polymer, 20 to 50 weight percent polyvinyl chloride polymer and 5 to 30 weight percent polycaprolactone polymer, with the term "weight percent" meaning exclusive of the weight of the other additives. Compositions which comprise 35 to 45 weight percent carboxylated nitrile rubber, 35 to 45 weight percent polyvinyl chloride and 10 to 20 weight percent polycaprolactone are preferred.
The process of the present invention requires the use of a peroxy curing agent. The term "peroxy curing agent" as used herein is meant to refer to the well known peroxide and hydroperoxide curing agents.
Any of the conventional peroxy curing agents may be employed, including dicumyl peroxide, tertiary butyl peroxy benzoate, cumene hydroperoxide, 2,5 dimethyl-2,5 di(benzoyl peroxy) hexane, and benzoyl peroxide. The amount of peroxy curing agent should be from about 0.2 to 10 "parts by weight", wherein the term parts by weight refers to its conventional meaning, namely parts by weight per 100 parts by weight of total polymer. The preferred amount will depend upon the specific type of peroxy curing agent chosen. Skilled persons will be able to readily optimize curatives, using small scale experiments with less than 100 grams of polymer.
The process of the present invention also requires the use of a crosslinking coagents. Any of the coagents which may be employed in peroxy curing reactions are suitable for use in the present invention. Examples of such coagents include triethylene glycol dimethacrylate, trialkyl cyanurate, trialkyl phosphate, ethylene dimethacrylate, 1.2 polybutadiene, zinc acrylate and tetrahydrofurfuryl methacrylate. The amount of the coagent is from 3 to 20 parts by weight, preferably 5 to 10 parts by weight. Mixtures of more than one coagent may also be employed.
The stabilizers used in the present invention may be one or more of the commercially available metal salts, organo metallic salts or soaps or organometallic compounds which are well known in the art. These stabilizers are frequently sold on a propietary basis, with their exact chemical composition not being disclosed. A description of available stabilizers which are used with PVC is given in Chapter 9 of "Encyclopedia of PVC", edited by L. I. Nass and published by Marcel Dekker Inc. Using the classification scheme described therein, suitable stabilizers for use in the present invention include lead salts, mixed metal salts, organotin stabilizers and organonickel stabilizers. Preferred stabilizers include the mixed metal salts of barium/cadmium, barium/cadmium/zinc, and barium/zinc and the organotin stabilizers. The total amount of stabilizers in a polymer blend for use in the process of the present invention is from about 1.0 to 4 parts by weight, preferably from about 1.5 to 3 parts by weight.
The antioxidants for use in the present invention may be one or more of any of the antioxidants which are used in the art of compounding heat resistant, carboxylated nitrile rubber. Suitable antioxidants include p-cumyldiphenylamide, octylated diphenylamine, polymerized 1,2 dihydro-2,2,4-trimethylquinoline, nickel salts of dibutyl- and dimethyl-dithiocarbamate, mercaptobenzimidazole and its zinc salts 2-mercaptobenzimidazole and its zinc salts, tris(nonylated phenyl)phosphite, p-phenylenediamine derivatives, and hindered phenolic antioxidants such as thiodiethylene bis(3,5-di-t-butyl-4-hydroxy)hydro cinnamate. The total amount of antioxidats used in compositions of the present invention is from about 0.2 to 4 parts by weight. A mixture of more than one antioxidant may be used.
The compositions prepared according to the present invention may optionally include further additives such as, for example, pigments, fillers, extender oils such as dioctyl phthalate and processing aids. The process of the invention is carried out by mixing the components in ordinary mixing equipment, such as mill roll mixers, banbury mixers, and screw mixers. The mixture is heated and kneaded at a temperature above the activation temperature of the peroxide. The temperature must be above the activation temperature of the peroxide in order for the dynamic curing reaction to proceed.
It is well known to skilled persons that excessive heat may degrade the polymers which are utilized in the process of the present invention. Therefore, the mixing process should not exceed about 210° C. The polymer composition is preferably mixed at a temperature of from about 145° to about 180° C., especially from about 160° to about 170° C.
Preferred mixing times are from about 2 to about 30 minutes, especially from about 3 to about 10 minutes.
The present invention is illustrated by the following, non-limiting examples.
In this and the following examples, the polymers used are identified in Table 1. The figures given are percent by weight.
TABLE 1
______________________________________
PVC A polyvinyl chloride sold under the trade name
Esso PVC 360 by Esso Chemical Canada.
XNBR A carboxylated nitrile rubber containing about 29
percent acrylonitrile and about 7 percent
carboxylic acid.
PP A polypropylene resin sold under the trade name
Himont 6331.
SB A block styrene-butadiene polymer sold under the
trade name Kraton TR 1101.
PolyCap
A polycaprolactone sold under the trade name CAPA
601P
EVA An ethylene-vinyl acetate resin sold under the
trade name Elvax 150.
______________________________________
Dynamically vulcanized compositions were prepared using the following procedure. Mixing was carried out in a labaoratory scale banbury mixer at 77 rpm. The ingredients shown in Table 2 were loaded at zero minutes with the banbury at a temperature of 82° C. and the heating steam on. Mixing was initiated and continued for a total time of 5-6 minutes. At a time when the mixing chamber temperature reached about 149° C., the ram was lifted and the banbury was brushed down. The dynamically cured compositions were dumped and sheeted using a laboratory mill mixer at a roll temperature of 120° C. The stock was then removed from the mill and allowed to cool.
Cooled stock was then comminuted in a dicing machine and fed to an injection molding machine. Injection molding was completed in a 50 ton press machine, using the following conditions:
locking pressure: 900 psi
injection pressure: 400 psi
Front zone temperature: 300° F.
Feed zone temperature: 270° F.
Dumbbell shaped samples were molded. Physical testing was carried out on the molded samples, according to ASTM D2240-81 (hardness); ASTM D412-80 (modulus, tensile strength and elongation); ASTM D395-78, at 70° C. (compression set), ASTM D1238 at 190° C. and 298.2 kPa (melt flow index) and ASTM D471-79 (fuel resistance).
Comparative experiment 1 illustrates a dynamically vulcanized blend containing PVC and carboxylated nitrile rubber. The compression set of the composition is good. However, the melt flow index is fairly low. Accordingly, the vulcanized composition of comparative experiment 1 may be characterized as being elastomeric, but it should not be regarded as a thermoplastic elastomer.
Inventive experiment 2 illustrates a dynamically vulcanized composition which displays a good balance between melt flow index and compression set. Thus, the physical properties of the composition of experiment 2, especially compression set, suggest a rubbery composition. In addition, the melt flow index shows that the composition may be readily molded or extruded.
TABLE 2
______________________________________
Experiment 1 2
______________________________________
Polymer Ingredients (weight percent)
XNBR 40 40
PVC 40 40
PolyCap -- 20
Additives (parts by weight)
Dicumyl peroxide 0.5 0.5
Tetrahydrofurfuryl methacrylate
10 10
Zinc acrylate 4 4
Di octyl phthalate 25 25
oi (butoxy-ethoxy-ethyl) formal
15 15
epoxidized soya bean oil
5 5
barium/cadmium stabilizer
2.5 2.5
zinc salt of 2-mercaptobenzimidazole
1.5 1.5
tris (nonylated phenyl) phosphite
0.5 0.5
thiodicthylene bis-(3,5-di-tert-butyl-4-hydroxy)
0.5 0.5
hydrocinnamate
calcium stearate 1.0 1.0
Melt Flow Index (g/10 min.)
5.7 29.3
Physical Properties
Hardness (Sore A) 67 71
100 modulus (MPa) 3.9 3.0
Tensile Strength (MPa) 12.8 6.8
Elongation at break (%) 340 270
Compression set (% after 70 hrs at 70° C.)
60 54
Aged in AST "Fuel C" (70 hrs at 23° C.)
Hardness 53 57
100% modulus 2.7 2.2
Tensile Strength 9.6 6.4
Elongation at break 330 320
% volume change 9 9
______________________________________
This example illustrates the dynamic vulcanization of compositions which contain polyvinyl chloride, carboxylated nitrile rubber and a third resin.
The compositions of Table 3 were prepared according to the mixing procedures of example 1.
The composition of comparative experiment 10 contains SB copolymer and exhibits a relatively low melt flow index.
The compositions of comparative experiments 11 and 13 utilize 20 weight percent polypropylene and ethylene-vinyl acetate, respectively. Both compositions have an excellent melt flow index. However, the compression set of both compositions is higher than the compression set of the composition of inventive experiment 12.
The composition of inventive experiment 12 demonstrates a good balance between melt flow index and compression set.
TABLE 3
______________________________________
Experiment 10 -C 11 -C 12 13 -C
______________________________________
Polymer Ingredients (weight
percent)
XNBR 40 40 40 40
PVC 40 40 40 40
SB 20 -- -- --
PP -- 20 -- --
Polycap -- -- 20 --
EVA -- -- -- 20
Additives (parts by weight)
Dicumyl peroxide 0.5 0.5 0.5 0.5
Tetrahydrofurfuryl methacrylate
10 10 10 10
Zinc acrylate 4 4 4 4
Dioctylphthalate 25 25 25 25
Di (butoxy-ethoxy-ethyl) formal
15 15 15 15
epoxidized soya bean oil
5 5 5 5
barium/cadmium stabilizer
2.5 2.5 2.5 2.5
zinc salt of 1.5 1.5 1.5 1.5
2-mercaptobenzimidazole
tris (nonylated-phenyl)
0.5 0.5 0.5 0.5
phosphite
calcium stearate 1.0 1.0 1.0 1.0
thiodiethylene bis-3,5-di-
0.5 0.5 0.5 0.5
tert-butyl-hydroxy
hydrocinnamate
Melt Flow Index (g/10 min)
2.1 >80 34.9 81.8
Physical Properties
Hardness (Shore A)
59 80 71 64
100% Modulus (MPa)
2.3 -- 3.2 2.7
Tensile Strength (MPa)
3.9 3.9 10.6 5.4
Elongation at Break (%)
190 60 360 220
Compression set (% after
58 65 47 56
70 hrs at 70° C.)
Aged in ASTM "Fuel C"
(70 hrs at 23° C.)
Hardness 36 67 45 38
100% modulus 1.7 2.4 1.7 1.5
Tensile Strength 1.7 2.6 7.2 2.2
Elongation at Break
100 120 320 150
% volume change 45 10 15 23
______________________________________
-C: comparative
This example illustrates the effect of using different amounts of peroxy curing agent.
Comparative experiment 20 was performed without any peroxide. Although the melt flow index of the resulting composition is excellent, the compression set is quite poor.
TABLE 4
______________________________________
20 21 22
Experiment (comparative)
______________________________________
Polymer Ingredients (weight percent)
XNBR 40 40 40
PVC 40 40 40
Additives (parts by weight)
Polycap 20 20 20
Dicumyl peroxide -- 0.5 1.0
Tetrahydrofurfuryl methacrylate
10 10 10
Zinc acrylate 4 4 4
Dioctyl phtalate 25 25 25
Di(butoxy-ethoxy-ethyl) formal
15 15 15
Epoxidized soya bean oil
5 5 5
barium/cadmium stabilizer
2.5 2.5 2.5
zinc salt of 2-mercaptobenzimidazole
1.5 1.5 1.5
tris nonylated phenyl phosphite
0.5 0.5 0.5
calcium stearate 1.0 1.0 1.0
thiodiethylene bis-(3,5-di-tert-
0.5 0.5 0.5
butyl-4-hydroxy) hydrocinnamate
Melt Flow Index (g/10 min)
43.8 29.3 19.5
Physical Properties
Hardness ("Shore A") 68 71 71
100% modulus (MPa) 1.9 3.0 3.3
Tensile Strengrh (MPa) 5.9 6.8 8.8
Elongation at Break (%)
550 270 310
Compression set (% after 70 hrs
71 60 54
at 70° C.)
Aged in ASTM "Fuel C" (70 hrs at 23° C.)
Hardness (Shore A) 43 57 54
100% modulus (MPa) 1.3 2.2 2.4
Tensile Strength (MPa) 4.9 6.4 6.1
Elongation at Break (%)
620 320 280
% volume change 10 9 8
______________________________________
Claims (3)
1. A vulcanizate comprising
(i) from 20 to 50 parts by weight carboxylated nitrile rubber and,
(ii) from 20 to 50 parts by weight polyvinyl chloride, and
(iii) from 5 to 30 parts by weight polycaprolactone, such that the total of said (i), said (ii) and said (iii) is 100 parts by weight, and
(iv) from 0.2 to 10 parts by weight peroxy curing agent,
(v) from 3 to 10 parts by weight coagent for said peroxy curing agent,
(vi) from 1 to 4 parts by weight stabilizer, and
(vii) from 0.2 to 4 parts by weight antioxidant, wherein said vulcanizate is obtained by admixing at a temperature above the actuation temperature of said peroxy curing agent, for a sufficient length of time to cause admixing and vulcanization but not cause significant thermal degradation of said carboxylated nitrile rubber, said polyvinyl chloride or said polycaprolactone.
2. The vulcanizate of claim 1 wherein said carboxylated nitrile rubber is a copolymer of butadiene, acrylonitrile and one or more α,β unsaturated carboxylic acids selected from the group consisting of methacrylic, fumaric, maleic and itaconic acids.
3. The vulcanizate of claim 1 wherein said peroxy curing agent is dicumyl peroxide and said coagent is a mixture of tetrahydrofurfuryl methacrylate and zinc methacrylate.
Priority Applications (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/119,099 US4826910A (en) | 1987-11-10 | 1987-11-10 | Oil resistant thermoplastic elastomer |
| CA000580082A CA1302605C (en) | 1987-11-10 | 1988-10-13 | Oil resistant thermoplastic elastomer |
| KR1019880014449A KR890008233A (en) | 1987-11-10 | 1988-11-03 | Thermoplastic elastomer with oil resistance |
| EP88118477A EP0317814B1 (en) | 1987-11-10 | 1988-11-05 | Oil resistant thermoplastic elastomer |
| DE8888118477T DE3871345D1 (en) | 1987-11-10 | 1988-11-05 | OIL RESISTANT THERMOPLASTIC ELASTOMER. |
| JP63281521A JPH01165638A (en) | 1987-11-10 | 1988-11-09 | Oil resistant thermoplastic elastomer composition and production thereof |
| IN783/MAS/88A IN171931B (en) | 1987-11-10 | 1988-11-09 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/119,099 US4826910A (en) | 1987-11-10 | 1987-11-10 | Oil resistant thermoplastic elastomer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US4826910A true US4826910A (en) | 1989-05-02 |
Family
ID=22382552
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/119,099 Expired - Lifetime US4826910A (en) | 1987-11-10 | 1987-11-10 | Oil resistant thermoplastic elastomer |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US4826910A (en) |
| EP (1) | EP0317814B1 (en) |
| JP (1) | JPH01165638A (en) |
| KR (1) | KR890008233A (en) |
| CA (1) | CA1302605C (en) |
| DE (1) | DE3871345D1 (en) |
| IN (1) | IN171931B (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5344864A (en) * | 1988-07-15 | 1994-09-06 | Denki Kagaku Kogyo Kabushiki Kaisha | Polyvinyl chloride thermoplastic elastomer composition |
| US5352498A (en) * | 1992-08-19 | 1994-10-04 | The Goodyear Tire & Rubber Company | Package for compounding rubber and compounded rubber |
| US6538071B1 (en) * | 1999-09-07 | 2003-03-25 | Bayer Aktiengesellschaft | Rubber mixtures for roller coatings |
| US20030181558A1 (en) * | 2000-05-12 | 2003-09-25 | Von Hellens Carl Walter | Rubber composition |
| US20030236333A1 (en) * | 2002-06-21 | 2003-12-25 | Adrian Rawlinson | Rubber mixtures containing copolymers for the production of tires |
| US7037982B2 (en) * | 2001-01-17 | 2006-05-02 | Bayer Aktiengesellschaft | Rubber mixtures for roll coverings |
| US20070055018A1 (en) * | 2005-09-06 | 2007-03-08 | Dirk Achten | Crosslinkable compositions, thermoplastic elastomers obtainable therefrom and their use |
| EP4015179A1 (en) * | 2020-12-21 | 2022-06-22 | Parker Hannifin Corp. | Readily processable, oil-resistant thermoplastic vulcanizates |
| EP4015178A1 (en) * | 2020-12-21 | 2022-06-22 | Parker Hannifin Corp. | Readily-processable, high-temperature, oil-resistant thermoplastic vulcanizates |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0730214B2 (en) * | 1991-12-10 | 1995-04-05 | クレハエラストマー株式会社 | Liquid composition for sealing |
| GB2271115A (en) * | 1992-07-14 | 1994-04-06 | Joseph Gordon Robinson | Low compression set glazing seals |
| US20070021564A1 (en) * | 2005-07-13 | 2007-01-25 | Ellul Maria D | Peroxide-cured thermoplastic vulcanizates |
| US7872075B2 (en) | 2005-10-07 | 2011-01-18 | Exxonmobil Chemical Patents Inc. | Peroxide-cured thermoplastic vulcanizates and process for making the same |
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| DE1063736B (en) * | 1956-10-19 | 1959-08-20 | Phoenix Gummiwerke Ag | Protective coatings for rubber articles |
| US3037954A (en) * | 1958-12-15 | 1962-06-05 | Exxon Research Engineering Co | Process for preparing a vulcanized blend of crystalline polypropylene and chlorinated butyl rubber |
| US3419511A (en) * | 1965-07-19 | 1968-12-31 | Atlantic Refining Co | Plasticized polyvinyl chloride compositions containing an acrylonitrile-butadiene rubber and flexible, oil resistant films and sheets produced therefrom |
| US3613613A (en) * | 1959-07-29 | 1971-10-19 | Continental Can Co | Closure member coating composition comprising an organosol-solution of polyvinyl chloride, acrylonitrile-butadiene copolymer, and phenolic resole resin |
| DE2650258A1 (en) * | 1976-11-02 | 1978-05-03 | Rehau Plastiks | USE OF AN ALLOY OF SOFT POLYVINYL CHLORIDE AND BUTADIENE ACRYLNITRILE MIXED POLYMER FOR THE MANUFACTURE OF JOINT TAPES FOR HIGH DEMANDS |
| US4438230A (en) * | 1982-11-29 | 1984-03-20 | Polysar Limited | Carboxylated nitrile rubber/PVC/nylon flux blends |
| US4594367A (en) * | 1985-04-01 | 1986-06-10 | Bata Limited | Antistatic composition and articles made therefrom |
| US4619971A (en) * | 1985-03-29 | 1986-10-28 | General Electric Company | Linear polyester resin blends with high impact resistance |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3274143A (en) * | 1963-11-12 | 1966-09-20 | Union Carbide Corp | Lactone polyesters as plasticizers for vinyl resins |
-
1987
- 1987-11-10 US US07/119,099 patent/US4826910A/en not_active Expired - Lifetime
-
1988
- 1988-10-13 CA CA000580082A patent/CA1302605C/en not_active Expired - Fee Related
- 1988-11-03 KR KR1019880014449A patent/KR890008233A/en not_active Application Discontinuation
- 1988-11-05 DE DE8888118477T patent/DE3871345D1/en not_active Expired - Fee Related
- 1988-11-05 EP EP88118477A patent/EP0317814B1/en not_active Expired - Lifetime
- 1988-11-09 JP JP63281521A patent/JPH01165638A/en active Pending
- 1988-11-09 IN IN783/MAS/88A patent/IN171931B/en unknown
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1063736B (en) * | 1956-10-19 | 1959-08-20 | Phoenix Gummiwerke Ag | Protective coatings for rubber articles |
| US3037954A (en) * | 1958-12-15 | 1962-06-05 | Exxon Research Engineering Co | Process for preparing a vulcanized blend of crystalline polypropylene and chlorinated butyl rubber |
| US3613613A (en) * | 1959-07-29 | 1971-10-19 | Continental Can Co | Closure member coating composition comprising an organosol-solution of polyvinyl chloride, acrylonitrile-butadiene copolymer, and phenolic resole resin |
| US3419511A (en) * | 1965-07-19 | 1968-12-31 | Atlantic Refining Co | Plasticized polyvinyl chloride compositions containing an acrylonitrile-butadiene rubber and flexible, oil resistant films and sheets produced therefrom |
| DE2650258A1 (en) * | 1976-11-02 | 1978-05-03 | Rehau Plastiks | USE OF AN ALLOY OF SOFT POLYVINYL CHLORIDE AND BUTADIENE ACRYLNITRILE MIXED POLYMER FOR THE MANUFACTURE OF JOINT TAPES FOR HIGH DEMANDS |
| US4438230A (en) * | 1982-11-29 | 1984-03-20 | Polysar Limited | Carboxylated nitrile rubber/PVC/nylon flux blends |
| US4619971A (en) * | 1985-03-29 | 1986-10-28 | General Electric Company | Linear polyester resin blends with high impact resistance |
| US4594367A (en) * | 1985-04-01 | 1986-06-10 | Bata Limited | Antistatic composition and articles made therefrom |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5344864A (en) * | 1988-07-15 | 1994-09-06 | Denki Kagaku Kogyo Kabushiki Kaisha | Polyvinyl chloride thermoplastic elastomer composition |
| US5352498A (en) * | 1992-08-19 | 1994-10-04 | The Goodyear Tire & Rubber Company | Package for compounding rubber and compounded rubber |
| US6538071B1 (en) * | 1999-09-07 | 2003-03-25 | Bayer Aktiengesellschaft | Rubber mixtures for roller coatings |
| US20030181558A1 (en) * | 2000-05-12 | 2003-09-25 | Von Hellens Carl Walter | Rubber composition |
| US7037982B2 (en) * | 2001-01-17 | 2006-05-02 | Bayer Aktiengesellschaft | Rubber mixtures for roll coverings |
| US20030236333A1 (en) * | 2002-06-21 | 2003-12-25 | Adrian Rawlinson | Rubber mixtures containing copolymers for the production of tires |
| US20070055018A1 (en) * | 2005-09-06 | 2007-03-08 | Dirk Achten | Crosslinkable compositions, thermoplastic elastomers obtainable therefrom and their use |
| EP1762593A1 (en) * | 2005-09-06 | 2007-03-14 | Lanxess Deutschland GmbH | Crosslinkable Compositions, thermoplastic elastomers obtained therefrom and their use |
| CN1974663B (en) * | 2005-09-06 | 2011-06-22 | 朗盛德国有限责任公司 | Crosslinkable compositions, thermoplastic elastomers obtained therefrom and their use |
| US8013070B2 (en) | 2005-09-06 | 2011-09-06 | Lanxess Deutschland Gmbh | Crosslinkable compositions, thermoplastic elastomers obtainable therefrom and their use |
| EP4015179A1 (en) * | 2020-12-21 | 2022-06-22 | Parker Hannifin Corp. | Readily processable, oil-resistant thermoplastic vulcanizates |
| EP4015178A1 (en) * | 2020-12-21 | 2022-06-22 | Parker Hannifin Corp. | Readily-processable, high-temperature, oil-resistant thermoplastic vulcanizates |
Also Published As
| Publication number | Publication date |
|---|---|
| KR890008233A (en) | 1989-07-10 |
| EP0317814A1 (en) | 1989-05-31 |
| JPH01165638A (en) | 1989-06-29 |
| IN171931B (en) | 1993-02-13 |
| EP0317814B1 (en) | 1992-05-20 |
| DE3871345D1 (en) | 1992-06-25 |
| CA1302605C (en) | 1992-06-02 |
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